EP1660291A2 - Procede de formation de revetement en plastique - Google Patents

Procede de formation de revetement en plastique

Info

Publication number
EP1660291A2
EP1660291A2 EP04781421A EP04781421A EP1660291A2 EP 1660291 A2 EP1660291 A2 EP 1660291A2 EP 04781421 A EP04781421 A EP 04781421A EP 04781421 A EP04781421 A EP 04781421A EP 1660291 A2 EP1660291 A2 EP 1660291A2
Authority
EP
European Patent Office
Prior art keywords
mold
plastic
casting
metal mold
cooling
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
EP04781421A
Other languages
German (de)
English (en)
Other versions
EP1660291A4 (fr
Inventor
Robert A. Grimmer
Dave Syphers
Denis Moore
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
International Automotive Components Group GmbH
Original Assignee
Collins and Aikman Automotive Co Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Collins and Aikman Automotive Co Inc filed Critical Collins and Aikman Automotive Co Inc
Publication of EP1660291A2 publication Critical patent/EP1660291A2/fr
Publication of EP1660291A4 publication Critical patent/EP1660291A4/fr
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C39/00—Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor
    • B29C39/22—Component parts, details or accessories; Auxiliary operations
    • B29C39/38—Heating or cooling
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00—Moulds or cores; Details thereof or accessories therefor
    • B29C33/34—Moulds or cores; Details thereof or accessories therefor movable, e.g. to or from the moulding station
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00—Moulds or cores; Details thereof or accessories therefor
    • B29C33/56—Coatings, e.g. enameled or galvanised; Releasing, lubricating or separating agents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/16—Cooling
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C39/00—Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor
    • B29C39/02—Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor for making articles of definite length, i.e. discrete articles
    • B29C39/04—Shaping by casting, i.e. introducing the moulding material into a mould or between confining surfaces without significant moulding pressure; Apparatus therefor for making articles of definite length, i.e. discrete articles using movable moulds not applied
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
    • B29C41/02—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor for making articles of definite length, i.e. discrete articles
    • B29C41/18—Slush casting, i.e. pouring moulding material into a hollow mould with excess material being poured off
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C41/00—Shaping by coating a mould, core or other substrate, i.e. by depositing material and stripping-off the shaped article; Apparatus therefor
    • B29C41/34—Component parts, details or accessories; Auxiliary operations
    • B29C41/46—Heating or cooling
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
    • B29C35/08—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation
    • B29C35/0805—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation using electromagnetic radiation
    • B29C2035/0822—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation using electromagnetic radiation using IR radiation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/16—Cooling
    • B29C2035/1691—Cooling using gas-liquid mixtures
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00—Moulds or cores; Details thereof or accessories therefor
    • B29C33/02—Moulds or cores; Details thereof or accessories therefor with incorporated heating or cooling means
    • B29C33/06—Moulds or cores; Details thereof or accessories therefor with incorporated heating or cooling means using radiation, e.g. electro-magnetic waves, induction heating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/26—Scrap or recycled material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0018—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds having particular optical properties, e.g. fluorescent or phosphorescent
    • B29K2995/002—Coloured
    • B29K2995/0021—Multi-coloured
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2031/00—Other particular articles
    • B29L2031/30—Vehicles, e.g. ships or aircraft, or body parts thereof
    • B29L2031/3005—Body finishings

Definitions

  • the present invention relates to an improved method for forming relatively thin plastic skins or shells from a mold surface using infrared heating and evaporative cooling. More particularly, the method relates to the efficient manufacture of thin thermoplastic shells or skins used as the outer surface for automotive interior trim products such as instrument panels, door panels, headrests, console covers, air bag doors, glove box doors and the like.
  • ASA, etc. next evolved to minimize waste in the slush process and produce skins of more uniform thickness.
  • a defined thickness of powder next to the heated mold surface melted and the unmelted powder was returned to a powder box for future use.
  • This modular process resulted in the need for fewer molds and allowed for rapid mold changes.
  • a further difficulty with stainless steel tubes welded onto the electroform molds was one of shortened mold life. The heat stresses that the nickel mold was exposed to during welding of the tubes to the mold resulted in mold cracking. To solve this, alternate means of heating the mold were explored. Dipping the electroform into a fluidized bed (U.S. Patent 4,946,663 to Takamatsu) or into a heat transfer medium was employed. Induction heating (U.S.
  • a hybrid method utilizing a robot and multiple stations is disclosed in U.S. Patent 4,755,333 to Gray (commonly assigned and incorporated herein by reference).
  • US Patent 4,623,503 to Anestis, et al which is directed at apparatus of this type is commonly assigned to the assignee of the present invention and included herein by reference.
  • What is needed is a process that provides rapid cycle times, uses low cost energy and requires a relatively inexpensive facility. Further, the process should heat and cool only the mold and plastic skin material that it contains, and accommodate the use of thin lightweight molds. Even further, this should be an environmentally friendly process with little noise and wasted heat, using process apparatus that can be converted from one mold/product shape to another rapidly to reduce process downtime.
  • the present invention addresses the deficiencies of the prior art by providing an efficient skin-forming process utilizing lightweight metal molds heated via infrared (IR) energy and cooled preferably through evaporation via a water/air mist spray. Since the IR energy is directed preferably at the backside of the mold utilizing heater elements that are contoured to match the shape of the mold, little heat is wasted and any heating of ducting and other peripheral equipment as well as the surrounding ambient area is eliminated. Since the molds are not subjected to other stresses (air pressure, etc.) than their own weight, thinner and therefore, more uniform electroformed molds can be used, further decreasing cycle time and any propensity to stress crack. Alternatively, the grained surface of the mold containing the plastic shell material may also be heated.
  • IR infrared
  • Evaporative cooling using the latent heat of vaporization of water (or other fluids), provides a significant reduction in cooling time, which is further enhanced by the thinner more uniform electroform, by the elimination of any duct work needed for cooling and by the atomization of the water spray.
  • any material which changes phase or state in the temperature range of the process described herein may be used to cool the mold.
  • a further embodiment includes the use of heat absorption/emissivity as a means to tune or balance the heat input into various areas of the electroformed mold.
  • thermoplastic materials are more sensitive or conducive to heating by IR energy through the use of additives that improve the heat absorptivity of the thermoplastic materials, further reducing cycle time.
  • This feature is employed when IR heating is directed at the open side of the shell toward the plastic as it is solidifying in the mold.
  • a material such as carbon black may be added to the thermoplastic material to enhance its heat absorptivity.
  • the casting process may be organized in a number of ways, by using an over-and- under conveyor holding a number of molds, or in a modular fashion, but preferably by utilizing 3-4 stations and a robot to manipulate the mold from preheat (A) to casting (B), and back to heating for fusing (A), then to cooling (C) and stripping as shown in the appended drawings.
  • the present invention is directed at a method of producing plastic articles, comprising preheating a metal mold having a mold contour using infrared energy from infrared energy heating elements that are formed to match said mold contour to establish a casting temperature, casting plastic material onto said preheated metal mold, fusing said plastic using infrared energy, cooling said metal mold by contacting said metal mold with a material which can change phase or state and removing the cast plastic article from said metal mold.
  • the present invention is directed at a method of producing plastic articles, comprising a metal mold that is positioned at a first heating station, wherein a metal mold having a mold contour is preheated using infrared energy from infrared energy heating elements that are formed to match said mold contour to establish a casting temperature, positioning said mold at a second station and casting plastic material onto said preheated metal mold, positiomng said mold at said first station and fusing said plastic using infrared energy, positioning said mold at a third station and cooling said metal mold by contacting said metal mold with a material which can change phase or state, positioning said mold at a fourth station and removing the cast plastic article from said metal mold.
  • the present invention is directed at an apparatus for products cast as plastic articles comprising;: (i) a metal mold to receive cast plastic material, said mold having a mold contour; (ii) infrared heaters to heat said mold to a desired casting temperature, said infrared heaters including infrared heating elements formed to match the contour of said mold; and (iii) a cooling device to deliver a material which can change phase or state.
  • Figure 1 is a flow chart describing the process steps of the present invention.
  • Figure 2 is an exemplary schematic drawing of a process sequence in accordance with the present invention.
  • Figure 3 is a sectional view of the contoured heating apparatus of the present invention.
  • Figure 4 is a sectional view of the contoured cooling apparatus of the present invention.
  • Figure 1 is a flow chart depicting the process steps used in the invention to produce plastic skins for automotive trim applications.
  • a thin electroformed nickel mold is preheated using electric infrared heaters and when the mold reaches the preferred powder casting temperature for the specific plastic powder being processed, the mold is filled with powder, by using a powder box which clamps onto the mold face and which, when inverted, fills the mold cavity with powder.
  • the mold is then rotated, generally around its major axis, to allow the powder to contact the exposed inner surface of the electroformed mold and melt on this heated surface.
  • the mold/powder box combination is inverted and any unmelted powder is allowed to fall back into the powder box which is then undamped and retracted.
  • the mold may then be subjected to additional IR heat to fuse the plastic layer on the mold surface.
  • the mold is then sprayed with a fine mist of water and air to cool its surface to the desired stripping temperature. Once the stripping temperature is reached, the cooled solid skin is removed and the next cycle initiated.
  • Liquid thermoplastic formulations such as plastisols or organisols can be processed in a like manner. Further, multiple plastic materials may be cast in layered or non-layered (that is, adjacent) disposition to provide unique properties or reduce cost (particularly for backing layers where regrind may be used). Figure 2 depicts this process in greater detail.
  • the apparatus may take the form of a moving or indexing line, a robot manipulator and multiple stations (as disclosed in 4,759,333 to Gray and incorporated herein by reference), or any other sequence that is consistent with Figures 1 and 2, including casting multiple layers of plastic, multiple types of plastic and foamed layers of thermoplastic to form skins or shells. More particularly, a metal mold preferably of nickel and most preferably of electro- formed nickel, is formed having the surface pattern (grain, texture, decoration) and contour desired for the final automotive skin or shell.
  • this electroformed mold is of a relatively uniform thickness between 0.050" and 0.400", more preferably between and including 0.100"-0.150", to minimize the weight of nickel to be heated and cooled and to minimize internal stresses on the mold.
  • Thinner molds are possible depending on their shape and on their ability to support their own weight and that of the powder which must fill the mold to adequately coat the mold surface to make a complete and uniform skin.
  • other compositions of metal molds may be used, including but not limited to, nickel-copper, beryllium-copper, stainless steel, etc.
  • Electric IR heaters are preferred, such as those available from Convectronics in Haverhill, Massachusetts, as the energy source in the casting process as they are not noisy, do not emit gaseous pollution and are readily shapeable, allowing the heating elements to be contoured to closely match each specific mold outer contour. Targeting a time duration of about one minute to heat the combined mold mass and powder covering its surface to the casting temperature, about 47 watts/in 2 of energy are needed. While wavelengths of 0.7 to 1000 microns (the infrared portion of the electromagnetic spectrum) may be used, it has been found that the most desirable infrared wavelength is 2.1-3.0 microns in order to generate sufficient output temperature (1275-2000 degrees F) yet provide a reasonable heater element life and minimize potential safety hazards.
  • a heater capable of generating 47 watts/in 2 output produced a consistent operating output temperature of 1450 degrees F.
  • infrared heating elements capable of generating at least about 20 watts/in , more preferably at least 30 watts/in , even more preferably at least 40 watts/in 2 , and in a most preferred embodiment, in the range of 45- 55 watts/in .
  • Tubular IR heater elements about 3/8 of an inch in diameter, made of an Inconel outer sleeve and an Inconel wire element packed with magnesium oxide inside the Inconel sleeve, provided the desired energy.
  • the tubular heaters were provided with cold ends which simplified mounting, and fiber washers were used to seal each end of the sleeve to allow moisture to vent.
  • the tubular heaters were bent in a pattern to closely conform to the backside of the electroformed mold and spaced from 0.01" to 5 inches off the back surface of the mold, but preferably 1-3 inches off the mold surface.
  • the tubular heaters are further spaced about 1-3 inches apart running along the mold to uniformly cover the surface of the mold to be heated.
  • the tube spacing may be in a lateral, longitudinal, diagonal, or any other pattern which provides a relatively uniform coverage of the backside of the mold. Shorter elements provide fewer issues with thermal expansion upon heating.
  • thermocouple may be installed on the front surface of the mold at a point of average mold thickness to sense the temperature and control the tubular heater elements.
  • the thermocouple is preferably embedded in the mold by drilling a hole and potting the end of the wire using silver solder.
  • each heater element was equipped with a thermocouple and independently controlled using a solid state relay coupled with a voltage regulator.
  • adjacent heater elements may be connected in series and sensed with a single thermocouple.
  • thermocouple By connecting a thermocouple to each heater element, if one heater starts to override the adjacent heater element, the thermocouple alerts the solid state controller which is programmed to reduce the voltage to that heater, preventing burnout.
  • a heater array is provided which yields a uniform and consistent temperature, is specific to each mold shape and is portable such that it can easily be exchanged when a new mold shape is used. Consequently, a most desirable heating source is provided having no moving parts and without the potential pollution issues of noise, heat and fumes.
  • electroformed mold in order to yield a more uniform skin or shell thickness, especially in complex and undercut shapes, the use of black body absorption/emissivity is employed.
  • Black paint capable of withstanding the temperatures encountered in the process was applied to the backside of the mold to aid in heat transfer.
  • Nickel has an emissivity of 0.11 while a glossy black paint surface has an emissivity of about 0.86 providing much greater IR heat absorption.
  • the plastic skin or shell being formed should be as uniform as possible, usually around 0.025- 0.040 inches in thickness, and in order to use as little powder as possible to cast each shell, heat balancing of the mold is necessary. This is usually carried out using thermography techniques first, to provide a uniform mold temperature by adjusting the shape of the heater elements as well as the distance from the back surface of the mold and the applied power level to each heater element.
  • shells are cast and sectioned and measured for thickness every inch or so in both x and y planes to yield a shell preferably between 0.025-.040 inches in thickness. It has been found that a fine tuning of the heat balance, and therefore shell thickness, can further be accomplished through the application of different shades of grayscale paint to the back of the mold surface. Particularly in areas of the mold which are thin (due to the complex geometry of the shape being electroformed) and in "waste" areas where little or no skin or shell is desired, such as might get trimmed out of openings in the final product or along peripheral edges, light colored shades of grey paint may be applied to reduce the heat absorbed (and therefore the thickness of shell formed due to the melting of less powder).
  • FIG 3 is a sectional view of the heating apparatus of the present invention.
  • An electroformed nickel mold 10 is placed under an IR heating apparatus 20.
  • IR heating elements 14 preferably run in a parallel array along the length (alternatively, the width) of the mold and are contoured to follow the mold's surface spaced off by up to a few inches to provide uniform heat.
  • the preferred heating apparatus further comprises an outer frame 12 for support, a reflection shield 16 for containing the energy and directing it towards the mold surface and a layer of K-wool insulation 18.
  • phase or change in state cooling such as evaporative cooling
  • evaporative cooling is preferably employed since it takes advantage of the latent heat absorbed by a change in phase of the cooling media. This reduces the problems previously encountered using ambient air for cooling, especially during seasonal extremes (summer heat).
  • the hot electroformed mold containing the cast shell was sprayed using air at about 100 psi to atomize chilled water forced through spray nozzles (such as Binks or DeNilbis).
  • FIG 4 is a sectional view of the evaporative cooling apparatus.
  • a frame 22 was constructed to follow the shape of the mold which allowed for rows of nozzles 24 to be installed along its length and width.
  • the nozzles 24 are preferably set to be evenly spaced apart and a consistent distance from the mold 10, including its ends, to provide uniform and rapid cooling.
  • the nozzles may be concentrated in an area of greater heat build-up, which may require additional cooling in order to optimize cycle time.
  • a robot manipulates the mold from heating station (A) after preheating (see Figure 2), to casting station (B), back to heating station (A) for fusing, and finally to cooling station (C).
  • Having the spray nozzles for cooling in a separate station (C) from heating (A) allows for longer nozzle life without clogging. It is further possible to treat the cooling Water for algae, bacteria and scale to maintain the condition of the spray nozzles and keep the surface of the mold clean.
  • FIG. 2 the process sequence will be described.
  • An electroformed nickel mold is placed under an IR heating unit in station A, described in Figure 2 at position 1, in an inverted fashion where the backside of the mold has been painted black to optimize absorptivity.
  • the IR heater elements which have been contoured to resemble the backside of the electroformed mold preferably direct infrared energy at the backside of the mold (see Figure 3).
  • a thermocouple is attached to the mold cavity surface.
  • the mold When the mold reaches the optimum casting temperature for the specific thermoplastic being cast (thermoplastic urethane, polyvinyl chloride, thermoplastic elastomer, thermoplastic olefin, acrylonitrile- styrene-acrylic, blends and alloys thereof and the like), the mold is moved to a casting station B, as shown in Figure 2 at position 2, where it is clamped to a powder box containing the thermoplastic powder. As the powder box/mold combination is rotated around its major axis, powder contacts the hot mold surface and melts to form a uniform plastic layer. After rotation of 20 seconds or so, the mold is inverted so that any excess powder falls into the powder box, which is then separated from the mold, and retracted.
  • thermoplastic urethane polyvinyl chloride, thermoplastic elastomer, thermoplastic olefin, acrylonitrile- styrene-acrylic, blends and alloys thereof and the like
  • the electroformed mold is next moved back to the IR heating station A, shown at position 3 in Figure 2, to complete the fusing process (generally a mold temperature of about 400 degrees F depending on the specific powder or liquid plastic being cast).
  • the mold is next moved to a cooling station C, shown in Figure 2 at position 4, where a mist of water and air is sprayed on either one or both of the front and back surfaces to cool the mold to a strip temperature of about 140-150 F (roughly 30-60 seconds).
  • the plastic shell is removed from the mold at station D, shown in Figure 2 at position 5, and a new cycle is initiated.
  • the mold after preheating, may be connected sequentially to multiple powder boxes followed by multiple heating cycles to melt successive layered or non-layered plastic material on to the mold surface.
  • a fourth mold station second casting station
  • a plurality of plastic materials may be cast in an accelerated processing environment. For example, the time for casting said first plastic material and said second plastic material is less than 3.0 minutes, as a consequence of the use of the IR heating elements which provide the ability to rapidly alter mold temperature.
  • the mold in about 80 seconds (more generally 1-2 minutes), cast a first material in about 20 seconds (more generally 10 - 40 seconds), return the mold to the preheat station for heating to a second temperature for a second plastic material over a period of about 15 seconds (more generally 10-45 seconds), and casting said second plastic material, again, over a period of about 20 seconds (more generally 10-45 seconds).
  • evaporative cooling is preferred here, any process using latent heat (that required to change phase or state) is acceptable, so that in addition to water, materials like liquid nitrogen, dry ice (CO2), etc. and combinations thereof may find use.
  • the spray nozzle pattern can be optimized by contouring the nozzle layout to resemble the mold contour and accommodate any variations in mold thickness.
  • the invention provides a new and improved method for producing thin plastic skins or shells from a liquid or powder casting process.
  • electric infrared heating By employing electric infrared heating, a simplified process requiring few molds, and much less ducting and conveying apparatus, and which emits significantly less noise and waste heat to the environment is achieved.
  • a heat balancing method to provide uniform mold temperature, and more uniform shell thickness and gloss uniformity is disclosed using black body absorptivity. The process may find particular use in countries where electricity is cheaper than propane or oil as a source of process heating.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Oral & Maxillofacial Surgery (AREA)
  • Thermal Sciences (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)
  • Moulding By Coating Moulds (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Vehicle Interior And Exterior Ornaments, Soundproofing, And Insulation (AREA)

Abstract

L'invention concerne un appareil et un procédé de production d'articles en plastique. Le procédé consiste à préchauffer un moule métallique possédant un contour de moule au moyen d'éléments chauffants infrarouges formés de manière qu'ils épousent la forme du moule et qu'une température de coulée soit atteinte, à couler une matière plastique sur la surface du moule métallique préchauffé, à faire fondre le plastique au moyen d'une énergie infrarouge, à refroidir le moule métallique au moyen du changement de phase ou d'état d'un matériau de refroidissement et à enlever l'article en plastique coulé dudit moule métallique.
EP04781421A 2003-08-15 2004-08-16 Procede de formation de revetement en plastique Ceased EP1660291A4 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US10/641,997 US7550103B2 (en) 2001-10-09 2003-08-15 Plastic skin forming process
PCT/US2004/026724 WO2005016613A2 (fr) 2003-08-15 2004-08-16 Procede de formation de revetement en plastique

Publications (2)

Publication Number Publication Date
EP1660291A2 true EP1660291A2 (fr) 2006-05-31
EP1660291A4 EP1660291A4 (fr) 2009-11-11

Family

ID=32508347

Family Applications (1)

Application Number Title Priority Date Filing Date
EP04781421A Ceased EP1660291A4 (fr) 2003-08-15 2004-08-16 Procede de formation de revetement en plastique

Country Status (6)

Country Link
US (1) US7550103B2 (fr)
EP (1) EP1660291A4 (fr)
JP (1) JP2007502721A (fr)
KR (1) KR20060079800A (fr)
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KR20060079800A (ko) 2006-07-06
EP1660291A4 (fr) 2009-11-11
WO2005016613A3 (fr) 2005-04-21
CA2535651A1 (fr) 2005-02-24
US20040113322A1 (en) 2004-06-17
WO2005016613A2 (fr) 2005-02-24
JP2007502721A (ja) 2007-02-15
US7550103B2 (en) 2009-06-23

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